CN117103532A - PCTFE fluororesin aftertreatment air flow drying device - Google Patents
PCTFE fluororesin aftertreatment air flow drying device Download PDFInfo
- Publication number
- CN117103532A CN117103532A CN202311380511.6A CN202311380511A CN117103532A CN 117103532 A CN117103532 A CN 117103532A CN 202311380511 A CN202311380511 A CN 202311380511A CN 117103532 A CN117103532 A CN 117103532A
- Authority
- CN
- China
- Prior art keywords
- pipe
- drying tank
- heat exchange
- tank
- pctfe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000001035 drying Methods 0.000 title claims abstract description 66
- 229920002493 poly(chlorotrifluoroethylene) Polymers 0.000 title claims abstract description 18
- 239000005023 polychlorotrifluoroethylene (PCTFE) polymer Substances 0.000 title claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000005485 electric heating Methods 0.000 claims description 21
- 238000007599 discharging Methods 0.000 claims description 17
- 238000005192 partition Methods 0.000 claims description 7
- 238000001514 detection method Methods 0.000 claims description 6
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 239000011347 resin Substances 0.000 abstract description 16
- 229920005989 resin Polymers 0.000 abstract description 16
- 230000000694 effects Effects 0.000 abstract description 4
- 238000012545 processing Methods 0.000 abstract description 4
- 238000009825 accumulation Methods 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000004743 Polypropylene Substances 0.000 description 6
- -1 polypropylene Polymers 0.000 description 6
- 229920001155 polypropylene Polymers 0.000 description 6
- 238000012856 packing Methods 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229920002313 fluoropolymer Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C37/00—Component parts, details, accessories or auxiliary operations, not covered by group B29C33/00 or B29C35/00
- B29C37/0092—Drying moulded articles or half products, e.g. preforms, during or after moulding or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2027/00—Use of polyvinylhalogenides or derivatives thereof as moulding material
- B29K2027/12—Use of polyvinylhalogenides or derivatives thereof as moulding material containing fluorine
- B29K2027/18—PTFE, i.e. polytetrafluorethene, e.g. ePTFE, i.e. expanded polytetrafluorethene
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The application discloses a PCTFE fluororesin post-treatment airflow drying device, which comprises a bottom frame, wherein a drying tank is arranged at one end of the top of the bottom frame, and a heat exchange tank is arranged at the other end of the top of the bottom frame; according to the application, the drying tank, the inner pipe, the feed back pipe and the auger are arranged, the interior of the drying tank is divided into two relatively independent spaces through the inner pipe with a mesh structure, hot air flows can pass through the inner pipe after entering the interior of the drying tank, during processing, a resin product is kept in the interior of the inner pipe, the rubber product in the bottom shell is continuously conveyed upwards to the top of the inner pipe again through the feed back pipe and the auger, then the rubber product naturally slides to the interior of the bottom shell along the spiral material separation baffle under the action of gravity, the backflow speed is reduced, and the operation is repeated, so that the rubber product can fully contact with air flow passing through the interior of the drying tank, the drying efficiency is improved, internal and external temperature differences caused by accumulation can be effectively avoided, and the drying effect is improved.
Description
Technical Field
The application relates to the technical field related to resin drying devices, in particular to a PCTFE fluororesin post-treatment air flow drying device.
Background
PCTFE fluororesin is a high-performance fluoroplastic material having good chemical resistance, heat resistance and mechanical properties under various extreme environments, and in order to ensure the quality and performance of PCTFE fluororesin products, it is often necessary to post-treat the same, and drying of the PCTFE fluororesin products is an important part of the post-treatment process, and it is necessary to use the same in combination with a resin drying device. Reference is made to publication No.: "CN219368205U", disclosed is "a polypropylene resin drying apparatus", comprising: drying device body, telescoping device and shake device, this patent is through being provided with telescoping device and shake device, when the polypropylene resin stoving is accomplished, through using the telescoping device, the cylinder drives and places the board and shift out from the drying device body, make things convenient for the workman to collect polypropylene resin, also make things convenient for the polypropylene resin that will dry to place on placing the board, and place the board and can dismantle conveniently and wash, just can use shake device, through starting servo motor, shake the piece and drive and place the board and shake from top to bottom, its effect is that can make the polypropylene resin surface even receive the stoving, the moisture vaporization of accelerating the polypropylene resin surface adhesion improves the efficiency of stoving, and improve work efficiency, and degree of automation is high.
In the conventional resin drying apparatus, it is generally required to place the PCTFE fluororesin product to be treated inside the dryer and to ensure uniform distribution of the resin product, so that an effective storage area inside the dryer needs to be increased, and in the drying process, a part of the resin product is always deposited at a position close to the inside, and the contact efficiency with the air flow is lower than that of the outer resin product, so that an internal and external temperature difference is easily caused, and when the outer resin product reaches a critical temperature, the resin product of the inner layer is easily not dried due to uneven contact with the air flow, thereby affecting the drying effect.
Disclosure of Invention
In view of the above, the present application aims at overcoming the drawbacks of the prior art, and it is a primary object of the present application to provide a PCTFE fluororesin post-treatment air flow drying device, so as to solve the problems that the air flow passing efficiency is affected by accumulation of vertical products inside the prior drying device, and the drying efficiency is affected by temperature difference easily formed inside the drying device.
In order to achieve the above purpose, the present application adopts the following technical scheme:
a PCTFE fluororesin post-treatment airflow drying device comprises a bottom frame, wherein a drying tank is arranged at one end of the top of the bottom frame, and a heat exchange tank is arranged at the other end of the top of the bottom frame;
further, a top cover is arranged at the top end of the drying tank, a bottom shell is arranged at the bottom of the drying tank, and a feeding pipe is arranged at the upper part of one side of the top cover; the bottom shell penetrates through the top of the bottom frame, and a discharging connector is arranged at the bottom of the bottom shell; the outer wall of the drying tank is provided with a temperature detection module;
further, a first air inlet pipe is arranged at the lower part of one side of the heat exchange tank, the first air inlet pipe is communicated with the air blower, and the air blower is arranged at one side of the top of the underframe; a first air outlet pipe is arranged at the upper part of one side of the heat exchange tank, and the first air outlet pipe is communicated with a second air inlet pipe in a matched connection way; the second air inlet pipe is communicated with the lower part of the drying tank, and the second air outlet pipe is arranged at the upper part of the drying tank.
Further, an inner pipe is arranged in the drying tank, and the inner pipe is of a mesh structure; a feed back pipe is arranged in the inner pipe, and the bottom of the feed back pipe is connected with the inner wall of the bottom shell;
further, a motor is arranged at the top end of the top cover, and an output shaft of the motor is connected with the top end of the auger; the auger is arranged in the feed back pipe, and the end cover is arranged at the bottom of the auger.
Further, the axial lead of the drying tank, the axial lead of the inner pipe and the axial lead of the material returning pipe are on the same vertical straight line, a material separating baffle is arranged between the inner pipe and the material returning pipe, and the material separating baffle is of a spiral structure;
further, the upper end and the lower end of the outer wall of the feed back pipe are respectively provided with an opening structure.
Further, the inner diameter of the bottom shell is decreased from top to bottom, the maximum inner diameter of the bottom shell is smaller than the inner diameter of the drying tank, and the axial lead of the bottom shell, the axial lead of the feeding pipe and the axial lead of the feed back pipe are all on the same vertical straight line;
further, the maximum inner diameter of the bottom shell is the same as the inner diameter of the inner pipe.
Further, the electric heating pipes are arranged in the heat exchange tank, a plurality of electric heating pipes are arranged at equal intervals, and meanwhile, the electric heating pipes are of a U-shaped structure;
further, heat exchange plates are arranged in the heat exchange tank, and a plurality of heat exchange plates are arranged at equal intervals;
further, each of the electric heating pipes penetrates through all the heat exchange plates.
Further, the clamping pieces are arranged in the end cover, three clamping pieces are arranged at equal angles relative to the vertical axis of the end cover, and the clamping pieces are connected with the end cover in a rotating way;
further, a spring piece is arranged between each clamping piece and the inner wall of the end cover, and each clamping piece is matched with a spring piece to form a rotating structure.
Further, a clamping wheel is arranged in the end cover, and the clamping wheel is arranged at the top end of the opening plate; the opening and closing plate is arranged at the top end of the closing plate, and the opening and closing plate is connected with the closing plate in a rotating way; the closing plate is arranged at the upper end of the interior of the discharging connector;
further, the axial lead of the end cover, the axial lead of the clamping wheel and the axial lead of the opening plate are all on the same vertical straight line.
Compared with the prior art, the application has obvious advantages and beneficial effects, and in particular, the technical scheme can be as follows:
1. according to the application, the drying tank, the inner pipe, the feed back pipe and the auger are arranged, the interior of the drying tank is divided into two relatively independent spaces through the inner pipe with a mesh structure, hot air flows can pass through the inner pipe after entering the interior of the drying tank, during processing, a resin product is kept in the interior of the inner pipe, the rubber product in the bottom shell is continuously conveyed upwards to the top of the inner pipe again through the feed back pipe and the auger, then the rubber product naturally slides to the interior of the bottom shell along the spiral material separation baffle under the action of gravity, the backflow speed is reduced, and the operation is repeated, so that the rubber product can fully contact with air flow passing through the interior of the drying tank, the drying efficiency is improved, internal and external temperature differences caused by accumulation can be effectively avoided, and the drying effect is improved.
2. In the application, the discharging connector and the end cover are arranged, three clamping pieces and three spring pieces are arranged in the end cover, the spring pieces are mutually clamped with the clamping wheels through the elasticity of the spring pieces under the state of stopping rotation and low-speed rotation of the auger, the clamping pieces can inwards extrude the spring pieces and shrink into the inner wall of the end cover under the action of inertia under the state of high-speed rotation, at the moment, the clamping pieces are disconnected with the clamping wheels, when the auger rotates clockwise and at low speed, the clamping pieces are matched with the clamping wheels to push the opening and closing plate to synchronously rotate clockwise until the opening and closing plate is pushed to be mutually closed, the communication between the bottom shell and the discharging connector is interrupted, so that rubber products stored in the bottom shell are prevented from being discharged through the discharging connector, and when discharging is needed, the auger is stopped from being converted into anticlockwise rotation through the clockwise rotation, the clamping wheels are matched with the opening and closing plate to synchronously rotate anticlockwise until the opening and closing plate are mutually overlapped, the bottom shell is communicated with the discharging connector again, and the rubber inside is pushed to be automatically rotated anticlockwise, the discharging efficiency is improved through the discharging connector, and the discharging efficiency is improved, and the processing efficiency is improved.
3. The application is provided with the electric heating pipes, the heat exchange plates, the air blower and the temperature detection module, wherein the electric heating pipes and the heat exchange plates are arranged in the heat exchange tank, the air is conveyed into the heat exchange tank by matching with the air blower, hot air is formed by fully contacting with the heat exchange plates, and then is injected into the drying tank.
In order to more clearly illustrate the structural features and efficacy of the present application, the present application will be described in detail below with reference to the accompanying drawings and examples.
Drawings
FIG. 1 is a schematic perspective view of the present application;
FIG. 2 is a side view of FIG. 1 of the present application;
FIG. 3 is a rear view of FIG. 1 of the present application;
FIG. 4 is a bottom view of FIG. 2 of the present application;
FIG. 5 is a schematic perspective view of a heat exchanger plate according to the present application;
FIG. 6 is a bottom view of FIG. 5 of the present application;
FIG. 7 is a rear view of FIG. 5 of the present application;
FIG. 8 is a plan side view of the present application;
FIG. 9 is a cross-sectional view taken along the direction A-A in FIG. 8 in accordance with the present application;
FIG. 10 is a schematic perspective view of an opening plate according to the present application;
FIG. 11 is a top view of FIG. 10 in accordance with the present application;
FIG. 12 is an enlarged view of the application at B in FIG. 9;
fig. 13 is an enlarged view of the present application at C in fig. 10.
The reference numerals are as follows:
1. the device comprises a bottom frame, a 2-drying tank, a 3-top cover, a 4-feeding pipe, a 5-temperature detection module, a 6-bottom shell, a 7-discharging connector, an 8-heat exchange tank, a 9-first air inlet pipe, a 10-blower, a 11-first air outlet pipe, a 12-second air inlet pipe, a 13-second air outlet pipe, a 14-inner pipe, a 15-feeding pipe, a 16-separating partition plate, a 17-motor, a 18-auger, a 19-end cover, a 20-clamping piece, a 21-spring piece, a 22-opening plate, a 23-clamping wheel, a 24-closing plate, a 25-electric heating pipe, a 26-heat exchange plate and a 27-connecting pipe.
Detailed Description
It should be noted that, without conflict, the embodiments of the present application and features of the embodiments may be combined with each other. The application will be described in detail below with reference to the drawings in connection with embodiments.
In order to make the present application better understood by those skilled in the art, the following description of the technical solutions of the present application will be made in detail, but not all embodiments of the present application are apparent to some embodiments of the present application, with reference to the accompanying drawings in the embodiments of the present application. All other embodiments, which can be made by those skilled in the art based on the embodiments of the present application without making any inventive effort, shall fall within the scope of the present application.
Referring to fig. 1 to 4, the drying device comprises a bottom frame 1, wherein a drying tank 2 is installed at one end of the top of the bottom frame 1, and a heat exchange tank 8 is installed at the other end of the top of the bottom frame 1; a top cover 3 is arranged at the top end of the drying tank 2, a bottom shell 6 is arranged at the bottom of the drying tank 2, and a feeding pipe 4 is arranged at the upper part of one side of the top cover 3; the bottom shell 6 penetrates through the top of the bottom frame 1, and a discharging connector 7 is arranged at the bottom of the bottom shell 6; the outer wall of the drying tank 2 is provided with a temperature detection module 5; a first air inlet pipe 9 is arranged at the lower part of one side of the heat exchange tank 8, the first air inlet pipe 9 is communicated with a blower 10, and the blower 10 is arranged at one side of the top of the underframe 1; a first air outlet pipe 11 is arranged at the upper part of one side of the heat exchange tank 8, and the first air outlet pipe 11 is communicated with a second air inlet pipe 12 by matching with a connecting pipe 27; the second air inlet pipe 12 is communicated with the lower part of the drying tank 2, and the upper part of the drying tank 2 is provided with a second air outlet pipe 13.
Specifically, the tail end of the feeding pipe 4 is provided with a sealing cover capable of being opened and closed, so that air flow leakage is avoided in the processing process.
As a further explanation of the present embodiment, the end of the second air outlet pipe 13 is provided with a turning joint for guiding the direction of the discharged air flow, and the end of the turning joint has a grid structure.
Referring to fig. 5 to 7, an inner tube 14 is disposed inside the drying tank 2, and the inner tube 14 has a mesh structure; a feed back pipe 15 is arranged in the inner pipe 14, and the bottom of the feed back pipe 15 is connected with the inner wall of the bottom shell 6; the top end of the top cover 3 is provided with a motor 17, and an output shaft of the motor 17 is connected with the top end of an auger 18; the auger 18 is arranged in the feed back pipe 15, and an end cover 19 is arranged at the bottom of the auger 18.
In particular, the inner tube 14 of mesh construction serves to block the rubber product while not blocking air flow.
As a further explanation of this embodiment, the end cap 19 rotates synchronously with the auger 18, and the axis of the end cap 19 and the axis of rotation of the auger 18 are on the same vertical line.
Referring to fig. 5 to 7, the axis of the drying tank 2, the axis of the inner tube 14 and the axis of the feed back tube 15 are on the same vertical line, a material separating partition 16 is disposed between the inner tube 14 and the feed back tube 15, and the material separating partition 16 is in a spiral structure; the upper and lower ends of the outer wall of the feed back pipe 15 are provided with opening structures.
Specifically, the opening structures at the two ends of the feed back pipe 15 are convenient for the rubber products to enter and exit, and the rubber products are driven to circularly flow in the inner pipe 14 by the auger 18 which is matched with the rotation.
As a further explanation of the present embodiment, the partition plate 16 is used to partition the inner space of the inner tube 14, and is used to guide the flow direction of the leaked rubber product, and reduce the backflow speed of the rubber product.
Referring to fig. 1 to 8, the inner diameter of the bottom shell 6 decreases from top to bottom, and the maximum inner diameter of the bottom shell 6 is smaller than the inner diameter of the drying tank 2, and the axis of the bottom shell 6, the axis of the feed pipe 4 and the axis of the feed back pipe 15 are all on the same vertical straight line; the maximum inner diameter of the bottom shell 6 is the same as the inner diameter of the inner tube 14.
In particular, the funnel-shaped bottom shell 6 serves to guide the plastic product towards the bottom of the return pipe 15.
As a further explanation of this embodiment, the inner tube 14 of the mesh structure can reduce the flow rate of the air flow entering the inner tube 14, and avoid the influence of the excessive flow rate of the air flow on the backflow of the rubber product.
Referring to fig. 5 to 7, an electric heating pipe 25 is installed in the heat exchange tank 8, and a plurality of electric heating pipes 25 are equally spaced, and meanwhile, the electric heating pipes 25 have a "U" shape; the heat exchange tank 8 is internally provided with heat exchange plates 26, and a plurality of heat exchange plates 26 are arranged at equal intervals; each of said electric heating tubes 25 extends through all heat exchanger plates 26.
Specifically, the heating power of each electric heating tube 25 can be independently controlled, and the temperature of the hot air formed in the heat exchange tank 8 is adjusted by controlling the heating power of the electric heating tube 25.
As a further explanation of the present embodiment, the heat exchanging fins 26 are used to increase the heat exchanging area of the electric heating tube 25 and improve the heat exchanging efficiency.
Referring to fig. 9 to 13, the end cover 19 is internally provided with three engaging members 20, wherein the engaging members 20 are equiangularly arranged about a vertical axis of the end cover 19, and the engaging members 20 are rotationally connected with the end cover 19; a spring piece 21 is installed between each of the engaging members 20 and the inner wall of the end cover 19, and each of the engaging members 20 cooperates with one of the spring pieces 21 to form a rotating structure.
Specifically, the spring piece 21 pushes the engaging piece 20 to pop up the inner wall of the end cover 19 through the elasticity of the spring piece, and the engaging wheel 23 is pushed to rotate through the engaging piece 20.
As a further illustration of this embodiment, each of the snap members 20 is provided with an arcuate flange at its distal end.
Referring to fig. 12 and 13, the end cap 19 has an engaging wheel 23 inside, and the engaging wheel 23 is mounted on the top end of the opening plate 22; the opening and closing plate 22 is arranged at the top end of the closing plate 24, and the opening and closing plate 22 is connected with the closing plate 24 in a rotating way; the closing plate 24 is arranged at the upper end of the interior of the discharging connector 7; the axial lead of the end cover 19, the axial lead of the clamping wheel 23 and the axial lead of the opening and closing plate 22 are all on the same vertical straight line.
Specifically, the opening and closing plate 22 is stacked on the top end of the closing plate 24, and a limiting groove for limiting the rotation angle of the opening and closing plate 22 is formed in the top of the closing plate 24, and the rotation angle range of the opening and closing plate 22 is 0-80 degrees.
As a further explanation of the present embodiment, the communication state between the bottom case 6 and the discharge connector 7 is regulated by rotating the opening plate 22.
The working principle of the application is as follows: when in use, firstly, an internal power supply is connected, a motor 17 is started, a packing auger 18 and an end cover 19 are driven to synchronously rotate clockwise, at the initial stage of starting, when the packing auger 18 and the end cover 19 rotate at a low speed, a clamping piece 20 is driven to push a clamping wheel 23 to synchronously rotate until an opening plate 22 is driven to synchronously rotate and be mutually staggered with a closing plate 24 to be closed, then the clamping wheel 23 and the closing plate 24 stop rotating, as the rotating speed of the packing auger 18 and the end cover 19 increases, under the action of inertia, the clamping piece 20 presses a spring piece 21 and contracts to the inner wall of the end cover 19, then rubber products to be dried are poured into an inner pipe 14 through a feed pipe 4, then an electric heating pipe 25 and a blower 10 are started, the blower 10 drives air flow to be injected into a heat exchange tank 8 through a first air inlet pipe 9, and after the air entering the heat exchange tank 8 contacts the electric heating pipe 25 and the heat exchange plate 26, hot air flow is formed, then discharged through the first air outlet pipe 11 and injected into the drying tank 2 through the connecting pipe 27 and the second air inlet pipe 12, hot air flows into the inner pipe 14 and is discharged through the second air outlet pipe 13 after fully contacting with rubber products, the rubber products collected at the bottom of the inner side of the bottom shell 6 are driven by the clockwise rotating auger 18 to reflow back to the top end of the inner pipe 14 again, so that the rubber products fully contact with the hot air flows, the temperature inside the drying tank 2 is monitored in real time through the temperature detection module 5 in the drying process, after the drying is finished, the blower 10 and the electric heating pipe 25 are firstly closed, the motor 17 is then closed and the motor 17 is restarted, the auger 18 is driven to rotate anticlockwise, the clamping piece 20 is driven to push the clamping wheel 23 to rotate synchronously when the auger 18 and the end cover 19 rotate at a low speed at the initial stage of starting, until the opening plate 22 is driven to synchronously rotate and mutually overlap with the closing plate 24, the bottom shell 6 is communicated with the discharging connector 7 again, and then the rubber product stored in the bottom shell 6 is pushed to be discharged through the discharging connector 7 in an accelerating way under the action of the auger 18 rotating anticlockwise.
The foregoing description is only a preferred embodiment of the present application, and is not intended to limit the technical scope of the present application, so any minor modifications, equivalent changes and modifications made to the above embodiments according to the technical principles of the present application are still within the scope of the technical solutions of the present application.
Claims (8)
1. A PCTFE fluororesin aftertreatment air flow dryer, characterized in that: the drying device comprises a bottom frame (1), wherein a drying tank (2) is arranged at one end of the top of the bottom frame (1), and a heat exchange tank (8) is arranged at the other end of the top of the bottom frame (1);
a top cover (3) is arranged at the top end of the drying tank (2), a bottom shell (6) is arranged at the bottom of the drying tank (2), and a feeding pipe (4) is arranged at the upper part of one side of the top cover (3); the bottom shell (6) penetrates through the top of the bottom shell (1), and a discharging connector (7) is arranged at the bottom of the bottom shell (6); the outer wall of the drying tank (2) is provided with a temperature detection module (5);
a first air inlet pipe (9) is arranged at the lower part of one side of the heat exchange tank (8), the first air inlet pipe (9) is communicated with a blower (10), and the blower (10) is arranged at one side of the top of the underframe (1); a first air outlet pipe (11) is arranged at the upper part of one side of the heat exchange tank (8), and the first air outlet pipe (11) is communicated with a second air inlet pipe (12) in a matched connection pipe (27); the second air inlet pipe (12) is communicated with the lower part of the drying tank (2), and the second air outlet pipe (13) is arranged at the upper part of the drying tank (2).
2. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 1, wherein: an inner pipe (14) is arranged in the drying tank (2), and the inner pipe (14) is of a mesh structure; a feed back pipe (15) is arranged in the inner pipe (14), and the bottom of the feed back pipe (15) is connected with the inner wall of the bottom shell (6);
the top end of the top cover (3) is provided with a motor (17), and an output shaft of the motor (17) is connected with the top end of the auger (18); the auger (18) is arranged in the feed back pipe (15), and an end cover (19) is arranged at the bottom of the auger (18).
3. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 1, wherein: the axial lead of the drying tank (2), the axial lead of the inner pipe (14) and the axial lead of the feed back pipe (15) are on the same vertical straight line, a material separating partition plate (16) is arranged between the inner pipe (14) and the feed back pipe (15), and the material separating partition plate (16) is of a spiral structure;
the upper end and the lower end of the outer wall of the feed back pipe (15) are respectively provided with an opening structure.
4. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 1, wherein: the inner diameter of the bottom shell (6) is decreased from top to bottom, the maximum inner diameter of the bottom shell (6) is smaller than the inner diameter of the drying tank (2), and the axial lead of the bottom shell (6), the axial lead of the feeding pipe (4) and the axial lead of the feeding pipe (15) are all on the same vertical straight line;
the maximum inner diameter of the bottom shell (6) is the same as the inner diameter of the inner tube (14).
5. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 1, wherein: the electric heating pipes (25) are arranged in the heat exchange tank (8), the electric heating pipes (25) are arranged at equal intervals, and meanwhile, the electric heating pipes (25) are of a U-shaped structure.
6. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 5, wherein: the inside of the heat exchange tank (8) is provided with heat exchange plates (26), and a plurality of heat exchange plates (26) are arranged at equal intervals;
each of the electric heating pipes (25) penetrates through all the heat exchange plates (26).
7. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 2, wherein: the inside of the end cover (19) is provided with the clamping pieces (20), the clamping pieces (20) are arranged at equal angles relative to the vertical axis of the end cover (19), and meanwhile, the clamping pieces (20) are connected with the end cover (19) in a rotating way;
a spring piece (21) is arranged between each clamping piece (20) and the inner wall of the end cover (19), and each clamping piece (20) is matched with one spring piece (21) to form a rotating structure.
8. The PCTFE fluororesin aftertreatment air dryer apparatus of claim 2, wherein: the inside of the end cover (19) is provided with a clamping wheel (23), and the clamping wheel (23) is arranged at the top end of the opening plate (22); the opening and closing plate (22) is arranged at the top end of the closing plate (24), and the opening and closing plate (22) is connected with the closing plate (24) in a rotating way; the closing plate (24) is arranged at the upper end of the interior of the discharging connector (7);
the axial lead of the end cover (19), the axial lead of the clamping wheel (23) and the axial lead of the opening and closing plate (22) are all on the same vertical straight line.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202311380511.6A CN117103532B (en) | 2023-10-24 | 2023-10-24 | PCTFE fluororesin aftertreatment air flow drying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202311380511.6A CN117103532B (en) | 2023-10-24 | 2023-10-24 | PCTFE fluororesin aftertreatment air flow drying device |
Publications (2)
Publication Number | Publication Date |
---|---|
CN117103532A true CN117103532A (en) | 2023-11-24 |
CN117103532B CN117103532B (en) | 2023-12-26 |
Family
ID=88805990
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202311380511.6A Active CN117103532B (en) | 2023-10-24 | 2023-10-24 | PCTFE fluororesin aftertreatment air flow drying device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN117103532B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117283751A (en) * | 2023-11-27 | 2023-12-26 | 常州市星干干燥设备有限公司 | Fluororesin spin flash evaporation drying conveying equipment for ETFE powder drying |
Citations (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB585933A (en) * | 1944-05-10 | 1947-02-28 | Miles Lowell Edwards | Pump |
EP0653538A2 (en) * | 1993-11-12 | 1995-05-17 | Grupo Antolin-Ingenieria, S.A. | Cable type window winder with simplified kinematic chain and electrical or manual drive |
CN101776372A (en) * | 2010-01-28 | 2010-07-14 | 常州市星干干燥设备有限公司 | Nitrogen closed cycle drying and solvent recovery system |
EP2975347A1 (en) * | 2014-07-14 | 2016-01-20 | Bocchiotti S.p.A. Societa' per l'Industria Elettrotecnica | System for drying an extrudate exiting a calibration tank |
CN105962392A (en) * | 2016-05-29 | 2016-09-28 | 张玲玲 | Air cooling method for radix glycyrrhizae tea |
CN205668571U (en) * | 2016-06-06 | 2016-11-02 | 黑龙江科技大学 | A kind of high speed mine car automatic stopping wheel |
CN106541507A (en) * | 2016-12-09 | 2017-03-29 | 梅新星 | A kind of agitating type plastic raw materialss drying plant with accumulation of heat net |
CN206377974U (en) * | 2017-01-17 | 2017-08-04 | 定州市科瑞塑料制品有限公司 | A kind of batch mixing heater for being used to produce low smoke and zero halogen reworked material |
CN206459472U (en) * | 2017-01-05 | 2017-09-01 | 天津市鑫霞烘干设备制造有限公司 | A kind of layer-stepping high efficiency medicinal material dryer |
CN207022825U (en) * | 2017-07-25 | 2018-02-23 | 广东容祺智能科技有限公司 | A kind of crop pollinating device based on unmanned plane |
CN108327140A (en) * | 2017-12-22 | 2018-07-27 | 合肥善腾塑料科技有限公司 | A kind of plastic products processing drying unit |
CN108405193A (en) * | 2018-04-20 | 2018-08-17 | 湖州金丰粮油有限公司 | A kind of food inspection horizontal type screw settling centrifuge |
CN108592563A (en) * | 2018-04-18 | 2018-09-28 | 新乡市雷公饮片有限责任公司 | A kind of prepared slices of Chinese crude drugs drying machine |
CN109405516A (en) * | 2018-11-06 | 2019-03-01 | 马鞍山沐及信息科技有限公司 | A kind of medicinal material circulation drier |
CN109485482A (en) * | 2019-01-03 | 2019-03-19 | 倪晓燕 | A kind of straw organic fertilizer processing technology |
WO2019219041A1 (en) * | 2018-05-15 | 2019-11-21 | 山东名流餐处装备股份有限公司 | Kitchen waste processing method and processing apparatus |
CN210267950U (en) * | 2019-07-15 | 2020-04-07 | 四川恒远信友环境科技有限公司 | Heated air circulation oven of acoustic material production usefulness |
CN212488308U (en) * | 2020-05-12 | 2021-02-09 | 苏鹏 | Poultry fodder preprocessing device with drying function |
CN212806400U (en) * | 2020-07-02 | 2021-03-26 | 蒙城县虹升塑粉有限公司 | Energy-conserving drying device is used in processing of highlight powder coating |
CN112606208A (en) * | 2020-12-04 | 2021-04-06 | 李书华 | Numerical control full-automatic concrete foaming machine |
CN213208423U (en) * | 2020-09-07 | 2021-05-14 | 云南云景林纸股份有限公司 | Energy-saving drying waste heat recovery device |
CN213695570U (en) * | 2020-12-01 | 2021-07-16 | 文县文州国成茶业有限公司 | Drying machine beneficial to microbial fermentation of tea |
CN214027109U (en) * | 2020-11-10 | 2021-08-24 | 湖北金德包装有限公司 | Wrapping bag plastics feed arrangement |
CN215242144U (en) * | 2021-06-22 | 2021-12-21 | 鹤壁市天新电器有限公司 | Raw material particle drying device |
WO2022011933A1 (en) * | 2020-07-16 | 2022-01-20 | 安徽省华腾农业科技有限公司 | Agricultural machinery environmentally-friendly and efficient treatment device and method for straw |
CN114766420A (en) * | 2022-04-21 | 2022-07-22 | 湖南文理学院 | Aquaculture is with regulation and control device |
CN217636649U (en) * | 2022-05-17 | 2022-10-21 | 广东长信精密设备有限公司 | Particle drying device |
CN115534189A (en) * | 2022-10-13 | 2022-12-30 | 桐城市佳升包装有限公司 | Drying film forming device for processing chitosan-based antifogging antibacterial packaging film and working method thereof |
CN116832510A (en) * | 2023-07-10 | 2023-10-03 | 龙沃科技开发有限公司 | Filter for primary petroleum recovery |
-
2023
- 2023-10-24 CN CN202311380511.6A patent/CN117103532B/en active Active
Patent Citations (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB585933A (en) * | 1944-05-10 | 1947-02-28 | Miles Lowell Edwards | Pump |
EP0653538A2 (en) * | 1993-11-12 | 1995-05-17 | Grupo Antolin-Ingenieria, S.A. | Cable type window winder with simplified kinematic chain and electrical or manual drive |
CN101776372A (en) * | 2010-01-28 | 2010-07-14 | 常州市星干干燥设备有限公司 | Nitrogen closed cycle drying and solvent recovery system |
EP2975347A1 (en) * | 2014-07-14 | 2016-01-20 | Bocchiotti S.p.A. Societa' per l'Industria Elettrotecnica | System for drying an extrudate exiting a calibration tank |
CN105962392A (en) * | 2016-05-29 | 2016-09-28 | 张玲玲 | Air cooling method for radix glycyrrhizae tea |
CN205668571U (en) * | 2016-06-06 | 2016-11-02 | 黑龙江科技大学 | A kind of high speed mine car automatic stopping wheel |
CN106541507A (en) * | 2016-12-09 | 2017-03-29 | 梅新星 | A kind of agitating type plastic raw materialss drying plant with accumulation of heat net |
CN206459472U (en) * | 2017-01-05 | 2017-09-01 | 天津市鑫霞烘干设备制造有限公司 | A kind of layer-stepping high efficiency medicinal material dryer |
CN206377974U (en) * | 2017-01-17 | 2017-08-04 | 定州市科瑞塑料制品有限公司 | A kind of batch mixing heater for being used to produce low smoke and zero halogen reworked material |
CN207022825U (en) * | 2017-07-25 | 2018-02-23 | 广东容祺智能科技有限公司 | A kind of crop pollinating device based on unmanned plane |
CN108327140A (en) * | 2017-12-22 | 2018-07-27 | 合肥善腾塑料科技有限公司 | A kind of plastic products processing drying unit |
CN108592563A (en) * | 2018-04-18 | 2018-09-28 | 新乡市雷公饮片有限责任公司 | A kind of prepared slices of Chinese crude drugs drying machine |
CN108405193A (en) * | 2018-04-20 | 2018-08-17 | 湖州金丰粮油有限公司 | A kind of food inspection horizontal type screw settling centrifuge |
WO2019219041A1 (en) * | 2018-05-15 | 2019-11-21 | 山东名流餐处装备股份有限公司 | Kitchen waste processing method and processing apparatus |
CN109405516A (en) * | 2018-11-06 | 2019-03-01 | 马鞍山沐及信息科技有限公司 | A kind of medicinal material circulation drier |
CN109485482A (en) * | 2019-01-03 | 2019-03-19 | 倪晓燕 | A kind of straw organic fertilizer processing technology |
CN210267950U (en) * | 2019-07-15 | 2020-04-07 | 四川恒远信友环境科技有限公司 | Heated air circulation oven of acoustic material production usefulness |
CN212488308U (en) * | 2020-05-12 | 2021-02-09 | 苏鹏 | Poultry fodder preprocessing device with drying function |
CN212806400U (en) * | 2020-07-02 | 2021-03-26 | 蒙城县虹升塑粉有限公司 | Energy-conserving drying device is used in processing of highlight powder coating |
WO2022011933A1 (en) * | 2020-07-16 | 2022-01-20 | 安徽省华腾农业科技有限公司 | Agricultural machinery environmentally-friendly and efficient treatment device and method for straw |
CN213208423U (en) * | 2020-09-07 | 2021-05-14 | 云南云景林纸股份有限公司 | Energy-saving drying waste heat recovery device |
CN214027109U (en) * | 2020-11-10 | 2021-08-24 | 湖北金德包装有限公司 | Wrapping bag plastics feed arrangement |
CN213695570U (en) * | 2020-12-01 | 2021-07-16 | 文县文州国成茶业有限公司 | Drying machine beneficial to microbial fermentation of tea |
CN112606208A (en) * | 2020-12-04 | 2021-04-06 | 李书华 | Numerical control full-automatic concrete foaming machine |
CN215242144U (en) * | 2021-06-22 | 2021-12-21 | 鹤壁市天新电器有限公司 | Raw material particle drying device |
CN114766420A (en) * | 2022-04-21 | 2022-07-22 | 湖南文理学院 | Aquaculture is with regulation and control device |
CN217636649U (en) * | 2022-05-17 | 2022-10-21 | 广东长信精密设备有限公司 | Particle drying device |
CN115534189A (en) * | 2022-10-13 | 2022-12-30 | 桐城市佳升包装有限公司 | Drying film forming device for processing chitosan-based antifogging antibacterial packaging film and working method thereof |
CN116832510A (en) * | 2023-07-10 | 2023-10-03 | 龙沃科技开发有限公司 | Filter for primary petroleum recovery |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117283751A (en) * | 2023-11-27 | 2023-12-26 | 常州市星干干燥设备有限公司 | Fluororesin spin flash evaporation drying conveying equipment for ETFE powder drying |
CN117283751B (en) * | 2023-11-27 | 2024-02-06 | 常州市星干干燥设备有限公司 | Fluororesin spin flash evaporation drying conveying equipment for ETFE powder drying |
Also Published As
Publication number | Publication date |
---|---|
CN117103532B (en) | 2023-12-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN117103532B (en) | PCTFE fluororesin aftertreatment air flow drying device | |
CN104422265B (en) | Flat paddle dryer and flat paddle formula drying means | |
CN104132525A (en) | Powder material drying and cooling integrated device | |
KR20230104267A (en) | Infrared dehumidification, crystallization and drying integral barrel and crystallization drying integral | |
CN210415437U (en) | PERT floor heating pipe forming machine | |
CN211290868U (en) | Drying device for raw material processing | |
CN210374419U (en) | Reverse type material quick drying device | |
CN203518497U (en) | Flat paddle type dryer | |
CN206605760U (en) | A kind of water-cooled cable shaping device | |
CN110186264A (en) | A kind of rapeseed drying device | |
CN216080864U (en) | Drying device is used in flocculating agent production | |
CN104315826A (en) | Double-cyclone dryer | |
CN204085115U (en) | The dry cooling integration equipment of powder material | |
CN211204664U (en) | Drying device for clothing production | |
CN2896159Y (en) | Grain low-temeprature vacuum drying device | |
CN208465208U (en) | A kind of centrifugal spray dryer | |
CN205843264U (en) | Cabo hollow blade dryer | |
CN110372171A (en) | A kind of sludge dryer | |
CN221781182U (en) | Spray drying device of powder | |
CN221706054U (en) | Vacuum paddle graphite process dryer | |
CN211424896U (en) | Dehumidifying mechanism of fruit and vegetable dryer | |
CN217187929U (en) | Spray drying tower waste heat utilization equipment | |
CN214701666U (en) | Drying device of compound fertilizer anti-caking agent | |
CN221403826U (en) | Hollow blade dryer | |
CN210148711U (en) | Cooling device of cable material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |